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(Ann) #1
430 ENGINEERING THERMODYNAMICS

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\M-therm\Th9-2.pm5

Now cvCO 2 =

RCO 2
γ− 1
=
8 314
44 1 286 1

.
(. − ) [forCO.]Qγ^2 =1 286
= 0.661 kJ/kg K
and cpCO 2 = 1.286 × 0.661 = 0.85 kJ/kg K
For the mixture :

cp =

mc m c
mm

NCp Op
NCO

2 NC 2 2 O 2
22

+
+

=
4 1 039 6 0 85
46

×+×
+

..
() = 0.925 kJ/kg K. (Ans.)

cv =

mc m c
mm

NCvvO
NCO

2 NC 2 2 O 2
22

+
+

=

4 0 742 6 0 661
46

×+×
+

..
() = 0.693 kJ/kg K. (Ans.)
When the mixture is heated at constant volume :
Change in internal energy,
U 2 – U 1 = mcv(T 2 – T 1 ) = 10 × 0.693(50 – 20) = 207.9 kJ. (Ans.)
Change in entropy,
H 2 – H 1 = mcp(T 2 – T 1 ) = 10 × 0.925(50 – 20) = 277.5 kJ. (Ans.)
Change in entropy,

S 2 – S 1 = mcv loge T
T

2
1

+ mR loge V
V

2
1
= mcv loge
T
T

2
1

()QVV 12 =

= 10 × 0.693 × loge
273 50
273 20

+
+

F
HG

I
KJ
= 0.675 kJ/kg K. (Ans.)
When the mixture is heated at constant pressure :
If the mixture is heated at constant pressure ∆U and ∆H will remain the same.
The change in entropy will be

S 2 – S 1 = mcp loge

T
T

2
1


  • mR loge


p
p

2
1
= mcp loge
T
T

2
1

()Qpp 12 =

= 10 × 0.925 loge
323
293

F
HG

I
KJ = 0.902 kJ/kg K. (Ans.)
Example 9.11. A vessel of 1.8 m^3 capacity contains oxygen at 8 bar and 50°C. The vessel is
connected to another vessel of 3.6 m^3 capacity containing carbon monoxide at 1 bar and 20°C. A
connecting valve is opened and the gases mix adiabatically. Calculate :
(i)The final temperature and pressure of the mixture ;
(ii)The change of entropy of the system.
Take : For oxygen Cv = 21.07 kJ/mole K.
For carbon monoxide Cv = 20.86 kJ/mole K.

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